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    • 5. 发明授权
    • Exhaust gas purification device for an engine
    • 发动机废气净化装置
    • US06409973B1
    • 2002-06-25
    • US08523455
    • 1995-09-05
    • Yukio KinugasaToshifumi TakaokaKouhei IgarashiTakaaki Itou
    • Yukio KinugasaToshifumi TakaokaKouhei IgarashiTakaaki Itou
    • B01D5314
    • B01D53/9481B01D53/9495F01N3/0842F01N3/0871F01N3/0878F01N3/22F01N13/011F01N2270/00F01N2410/12F01N2610/03F01N2610/04F02B1/04
    • The exhaust gas purification device according to the present invention utilizes two NOx absorbents in order to remove NOx from the exhaust gas of an engine operated at a lean air-fuel ratio. The NOx absorbents are disposed, in series, in the exhaust passage of the engine and a nozzle for supplying a reducing agent is disposed in the exhaust passage at a position between the two NOx absorbents. Further, the device includes switching valves for changing the direction of the exhaust gas flow in the exhaust gas passage. When the switching valves are set to direct the exhaust gas flow to one direction, the exhaust gas first flows through one of the NOx absorbents (first NOx absorbent), and after passing through the first NOx absorbent, the reducing agent is supplied to the exhaust gas before it flows into the other NOx absorbent (second NOx absorbent). Thus, the first NOx absorbent absorbs NOx in the exhaust gas, and the NOx absorbed by the second NOabsorbent is released from the second NOx absorbent. When the switching valves are switched, the exhaust gas flows in the opposite direction, and flows through the second NOx absorbent and the first NOx absorbent in this order. In this case, the second NOx absorbent absorbs NOx in the exhaust gas, and the NOx absorbed by the first NOx absorbent is released and reduced to N2. Therefore, by reversing the direction of the exhaust gas periodically, the absorbing operation of NOx and releasing/reducing operation of NOx are performed by two NOx absorbents alternately. Thus, it becomes possible to remove NOx in the exhaust gas continuously while the NOx absorbents are prevented from being saturated by the absorbed NOx.
    • 根据本发明的排气净化装置利用两个NOx吸收剂来从以稀空燃比运转的发动机的废气中除去NOx。 NOx吸收剂串联设置在发动机的排气通道中,并且用于供给还原剂的喷嘴设置在排气通道中的两个NOx吸收剂之间的位置。 此外,该装置包括用于改变排气通道中的排气流的方向的切换阀。 当切换阀被设定为将废气流引导到一个方向时,废气首先流过NOx吸收剂之一(第一NOx吸收剂),并且在通过第一NOx吸收剂之后,还原剂被供给到排气 气体在其流入另一个NOx吸收剂(第二NOx吸收剂)之前。 因此,第一NOx吸收剂吸收废气中的NOx,并且由第二NO吸收剂吸收的NOx从第二NOx吸收剂释放。 当切换阀切换时,排气沿相反方向流动,并且依次流过第二NOx吸收剂和第一NOx吸收剂。 在这种情况下,第二NOx吸收剂吸收废气中的NOx,并且由第一NOx吸收剂吸收的NOx被释放并且还原成N2。 因此,通过周期性地反转排气的方向,NOx的吸收运转和NOx的释放/还原运转由两个NOx吸收剂交替进行。 因此,可以连续地除去排气中的NOx,同时防止NOx吸收剂被吸收的NOx饱和。
    • 8. 发明授权
    • Process for the reclamation of spent alkanolamine solution
    • 废链烷醇胺溶液回收方法
    • US06245128B1
    • 2001-06-12
    • US09333196
    • 1999-06-15
    • Joseph T. George, Jr.
    • Joseph T. George, Jr.
    • B01D5314
    • B01D53/526B01D53/1425B01J41/05B01J49/57
    • A process for the reclamation of spent aqueous alkanolamine solutions by contacting a spent aqueous alkanolamine solution with a strong base ion exchange resin for time sufficient to sorb from the aqueous alkanolamine solution at least a portion of the accumulated ions and after a high concentration of ions accumulate on the resin, regenerating the strong base ion exchange resin by: a) purging the resin with water or nitrogen, b) contacting the strong base ion exchange resin with a sodium chloride solution for a time sufficient to remove the ions, c) purging the resin to remove the sodium chloride solution, d) contacting the resin with an alkali metal hydroxide solution, preferably sodium hydroxide, for a time sufficient to convert the resin to a substantially hydroxide form; and e) purging the resin, wherein the ion sorption capacity of the resin is maintained at a substantially constant value.
    • 通过使废水性链烷醇胺溶液与强碱性离子交换树脂接触的时间足以从链烷醇胺溶液中吸收至少一部分积聚的离子并且在高浓度的离子积聚之后使废水性链烷醇胺溶液回收的方法 在树脂上,通过以下步骤再生强碱离子交换树脂:a)用水或氮吹扫树脂,b)使强碱离子交换树脂与氯化钠溶液接触足够时间以除去离子,c) 树脂以除去氯化钠溶液,d)使树脂与碱金属氢氧化物溶液(优选氢氧化钠)接触一段足以将树脂转化为基本氢氧化物形式的时间; 以及e)清洗树脂,其中树脂的离子吸附容量保持在基本恒定的值。
    • 9. 发明授权
    • Apparatus and method for producing HF from phosphate rock
    • 磷酸盐岩生产HF的设备及方法
    • US06179901B2
    • 2001-01-30
    • US09332085
    • 1999-06-14
    • Louis J. Lamb
    • Louis J. Lamb
    • B01D5314
    • B01D53/1456
    • Hydrogen fluoride production apparatus removes phosphate rock dust from a hot gas mixture exhausted from a phosphate rock defluorination kiln; cools the hot gas mixture in a heat exchanger to a low enough temperature that it can be brought into contact with acid-resistant polymeric materials without destroying them; uses a water spray scrubber for further cooling the gas and absorbing the fluoride values as HF-rich liquor; and pumps the HF liquor to a holding tank. One such plant uses a gas tube steam boiler as the heat exchange and has several series-connected scrubbers to extract the fluorine values from the kiln exhaust so that the residual gas mixture can be exhausted into the atmosphere without exceeding permissible fluorine value levels. In this arrangement water is fed into the scrubber furthest from the boiler to extract HF from the process gas, and an HF-laden process liquor is fed out of the furthest scrubber into the second furthest scrubber, where it is sprayed into the gas stream. This counter-current flow arrangement continues until one reaches the scrubber closest to the boiler and extracts the most concentrated process liquor from a sump nearest the boiler.
    • 氟化氢生产设备从磷酸盐岩脱氟窑排出的热气体混合物中除去磷酸盐岩粉尘; 将热交换器中的热气体混合物冷却到足够低的温度,使其能够与耐酸的聚合材料接触而不破坏它们; 使用喷水洗涤器进一步冷却气体并吸收作为富HF的液体的氟化物值; 并将HF液体泵送到储罐中。 一个这样的工厂使用气体管蒸汽锅炉作为热交换器,并且具有几个串联连接的洗涤器以从窑炉排气中提取氟值,使得残余气体混合物可以排放到大气中而不超过允许的氟值水平。 在这种布置中,水被送入距离锅炉最远的洗涤器中以从处理气体提取HF,并且将含HF的处理液从最远的洗涤器送出到第二最远的洗涤器中,在那里喷射到气流中。 这种逆流装置继续进行,直到到达最接近锅炉的洗涤器,并从最靠近锅炉的集水槽提取最浓缩的处理液。